US3923097A - Heat exchanger - Google Patents

Heat exchanger Download PDF

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Publication number
US3923097A
US3923097A US464642A US46464274A US3923097A US 3923097 A US3923097 A US 3923097A US 464642 A US464642 A US 464642A US 46464274 A US46464274 A US 46464274A US 3923097 A US3923097 A US 3923097A
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US
United States
Prior art keywords
helical
rotor
hollow space
hollow
rib
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US464642A
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English (en)
Inventor
Helge Hovad
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Atlas AS
Original Assignee
Atlas AS
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Filing date
Publication date
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Publication of US3923097A publication Critical patent/US3923097A/en
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Expired - Lifetime legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/18—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rotating helical blades or other rotary conveyors which may be heated moving materials in stationary chambers, e.g. troughs
    • F26B17/20—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rotating helical blades or other rotary conveyors which may be heated moving materials in stationary chambers, e.g. troughs the axis of rotation being horizontal or slightly inclined
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/90—Heating or cooling systems
    • B01F35/95—Heating or cooling systems using heated or cooled stirrers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/28—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rollers or discs with material passing over or between them, e.g. suction drum, sieve, the axis of rotation being in fixed position
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00—Heating arrangements
    • F26B23/10—Heating arrangements using tubes or passages containing heated fluids, e.g. acting as radiative elements; Closed-loop systems
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05—Stirrers
    • B01F27/11—Stirrers characterised by the configuration of the stirrers
    • B01F27/115—Stirrers characterised by the configuration of the stirrers comprising discs or disc-like elements essentially perpendicular to the stirrer shaft axis
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00—Heat exchange
    • Y10S165/135—Movable heat exchanger
    • Y10S165/139—Fully rotatable

Definitions

  • F28C 17/00 tionary drum with an internal hollow shaft or rotor [58] Field of Search 34/108, 109, 179-182, with means for circulating heating or cooling medium, ,34/134, 138, 139; 165/87, 88, 89, 92 said rotor being encircled by annular bodies in the shape of ribs with a helical, hollow space, the inner [56] References Cited end of which communicates with the interior of the UNITED STATES PATENTS rotor, the outer end being closed.
  • This invention relates to an apparatus in the shape of a heat exchanger for indirect heating, drying or cooling of moist tacky material, said apparatus being of the kind having a stationary drum with a revolving hollow shaft or rotor with an inlet for adrying medium and an outlet for the same or a condensate thereof, the rotor carryingannular bodies with cavities connected to the hollow space of the rotor.
  • An apparatus of the said kind will specifically be useful in thedrying of fishmeal, offal from slaughterhouses, mash from breweries, and the like tacky material of animal or vegetable origin.
  • drum driers with longitudinal pipes have been used, wherein the drum and the pipes rotate together or, as according to 'the Norwegian Pat. No. 62.174, the drums are stationary being fitted with also stationary heating pipesv coiled in planes perpendicular to the drumaxis, and with rotating stirring members mounted upon a central shaft, and moving between the coils.
  • the heating pipes are helically-coiled and mounted upon a rotating hollow shaft.
  • the cross-sectionally triangular design ofthe annular bodies makes them bulky so that only a limited number of bodies can find room on thejhollow rotor,
  • the object of the invention is to provide a dryer substantially relieving'the said disadvantages, being constructionally so designed that the manufacture thereof 2 can be largely mechanized and automatically carried through.
  • the characteristic feature of the drier of the invention is that the annular bodies encircling the rotor are designed as ribs with a helical hollow space, the inner end of which is in connection with the interior of the rotor, the outer end near the circum- I ference of the rib being closed.
  • This.de sign is based upon the recognition that the heat transmission number between heating surface and dryinggoods forthe materials dealt with here is so low, 20-60 kcal/m hC, that a fin or rib design asstated hereinbefore, where only part of the surface is directly heated, is effective. Owing to the small cross-sectional area of the heating coil and its confinement within curved surfaces, it will endure a relatively high pressure.
  • the heating coil is preferably of lenticular cross-section, the thickness of the individual annular body is small, and this, and the reduced weight on account of the reducedconsumption of rib material, has the effect that additional annular bodies can find room upon the hollow rotor without overloading the latter and without reducing the available space for material to be dried too much.
  • the ad-- made from a coiled tube being cut into halves along an axial plane.
  • the space between individual turns of the coil can be'reduced to a minimum by forming the strip used for making the helical hollow space from a sheet, in which only a single helical cut is made. The distance between the'individual turns will then correspond to the reduction in width resulting from the curving of the strip plus the width of the coil, and you get the largest possible area of the rib, which is in direct contact with the heating medium.
  • the above described embodiment may be changed so that the outer end of the helical hollow space according to the invention is connected with a radially extending return passage to the hollow space of the rotor through an opening in the plane rib sheet.
  • the flow rate of the heat medium can be increased, resulting in a larger heat transmission.
  • the heat transmission can be further increased in another embodiment according to the inventiomby ahelical strip 'of curved cross-section being mounted on each side of the plane sheet from which the rib is made.
  • the outer ends of the helical, hollow spaces can overlap
  • the stiffness of the rib sheet, and the capacity of withstanding internal pressure can be increased in a which the rib is made, said bulb being covered by a helically cut, and also embossed strip to form the helical hollow space.
  • this problem is solved by the provision in the helical hollow space of a more or less tight-fitting guide plate consisting of a correspondingly helical strip terminating shortly before the closed outer end of the hollow space.
  • This strip is only tightly fastened in part to allow the condensate to pass between the strip and the inner side of the heating coil.
  • the condensate will mainly be collected in the outer hollow space, where it is concurrent to the vapour. In this manner, the condensate and the air is more easily chased out of the heating coil.
  • the direction of rotation is preferably chosen so that the condensate is screwed towards the shaft.
  • a tube may be used, which is inserted in the hollow space of the heating coil. By means of this tube, the heating medium may be led forward to the outer end of the heating spiral.
  • an embodiment of the dryer may advantageously be designed so that the distance between the turns of the helical hollow space is adjusted so that helically cut strips can be used for forming the hollow spaces, said strips being substantially of a width corresponding to the distance between the turns of these helical strips.
  • the construction work consisting mainly in sheet cutting and welding, is well suited for automatizing owing to the long cuts and continuous welding seems. Further, the design of the fins or ribs results in a good utilization of the construction material, allowing for use of a more costly material, e.g. rustproof steel.
  • FIG. 1 schematically shows a longitudinal section of the drier
  • FIG. 2 on a larger scale an elevation of a rib on the hollow rotor of the apparatus, said rotor being seen in cross-section,
  • FIG. 3 a radial section through a rib
  • FIG. 4 a radial section through another embodiment of a rib
  • FIG. 5 an elevation of part of a rib as shown in FIG. 4,
  • FIG. 6 a section along the line AA in FIG. 5.
  • the drier schematically shown in FIG. 1 consists of a stationary drum 10, having a heating jacket 11 around its cylindrical part, an inlet 12 for the material to be dried, and an outlet 13, which is here placed at the bottom, but may also be placed some way up the side of the drum.
  • a rotor 14 having hollow axle-necks l5 and 16.
  • axle-neck 15 Through the axle-neck 15 passes a supply pipe 17 for the heating medium, here supposed to be steam, and through the axle-neck 16 a siphon pipe 18 is inserted for draining off condensate, respectively heating medium, if the latter does not condensate.
  • the heating medium here supposed to be steam
  • a siphon pipe 18 is inserted for draining off condensate, respectively heating medium, if the latter does not condensate.
  • the rotor 14 is fitted with ribs 19 having a smooth, but not plane exterior.
  • the said ribs may be of the design shown in elevation in FIG. 2 and in cross-section in FIG. 3 as having a helical duct 20 for the heating medium, said duct being connected at its inner end with the hollow space of the rotor 14 through a length of pipe 21.
  • the duct 20 is of lenticular or spindleshaped cross-section in the outer turns, see FIG. 3, whereas the turn adjacent the rotor is of substantially triangular cross-section with a generatrix for the rotor wall as base.
  • the rib 19 has been cut from a plane metal sheet, after which a substantially helical bulb has been embossed or caelered into the sheet, and the resulting depression is covered with a strip 22, which has been helically cut out and embossed to an arcuate cross-section, said strip being welded on to form the duct 20.
  • the duct 20 may be longitudinally divided almost onto the closed end by means of a coiled strip 23 being part-welded along one or both borders to the middle of the passage 20.
  • the strip 23 extends to contact with, and is possibly fixed onto the exterior of the rotor 14 behind the supply pipe 21 for the heating medium.
  • the medium is forced to first flow on to the extreme end of the duct 20 through that part of the said duct being closer to the rotor. It can then pass around the end of the partition formed by the strip 23 and return through the other part of the duct 20.
  • Possibly formed condensate will thus be driven forward by the heating medium and more easily returns to the hollow space of the rotor, from where it can be removed through the siphon pipe 18. More important is, however, that possibly separated air is also carried along and does not become stationary to form air pockets inhibiting or stopping the heating medium from entering the duct 20.
  • Condensate and air are returned to the rotor through a pipe 24. Just behind said pipe, a closed partition 25 is provided.
  • shovels 26 may be mounted crosswise to aid in moving the material to be dried forward towards the outlet 13.
  • the rotation of the rotor should be in such direction that the closed end of the duct 20 is in front so that the movement of the condensate back to the hollow space of the rotor is aided by the rotor movement, as shown by directional arrow A on FIG. 2 of the drawing.
  • the supply pipe 21 projects some way into the hollow space of the rotor so that its inner end will always be above the condensate level in the rotor space, said level being controlled by the siphon pipe 18.
  • each of the ribs 19 consists of a plane sheet to which has been welded the helically cut, and to an arcuate form embossed strip 22 to form the helical duct 20. Adjacent the closed outer end of the said duct, an opening 27 leads to a radial passage 28 on the backside of the rib 19, so that the condensate may be returned through this passage to the interior of the rotor 14.
  • a heat exchanger for treating moist, tacky material which comprises:
  • a stationary drum having b. an internal hollow shaft or rotor with inlet and outlet for the heat exchanging medium,
  • annular bodies in the shape of ribs encircling said rotor, each of said ribs being provided with a helical, hollow space, the inner end of which communicates with the hollow shaft, the outer end being closed, each said rib formed from a plane sheet,
  • Y and the helical hollow space thereof being formed by attachment to the sheet of a helically cut strip of arcuate cross-section, and means for rotating said hollow shaft and the shaft attached annular rib shaped bodies in a direction such'that the closed end of the helical space is in front whereby movement of the condensate back to the hollow space of the rotor is aided by the rotor movement.
  • Heat exchanger according to claim 1 in which a helical strip of curved cross-section is mounted on each side of the plane sheet, from which the rib is made, to form two helical hollow spaces in the rib.
  • Heat exchanger according to claim 2 in which the outer ends of the helical hollow spaces overlap one another and are mutually connected through an opening in the rib sheet.
  • Heat exchanger in which a helical bulb is embossed or calandered in the sheet, from which the rib is made, said bulb being covered by a helically cut, and also embossed strip to form the helical hollow space.
  • Heat exchanger according to claim 1 including a radially extending return passage, one end of said return passage connected to the outer end of the helical hollow space and the other end connected to the hollow space of the rotor.
  • a heat exchanger for treating moist, tacky material which comprises:
  • a stationary drum having b. an internal hollow shaft or rotor with inlet and outlet for the heat exchanging medium,
  • annular bodies in the shape of ribs encircling said rotor, each of said ribs being provided with a helical, hollow space, the inner end of which communicates with the hollow shaft, the outer end being closed, means for rotating said hollow shaft and the shaft attached annular rib shaped bodies, and a guide plate fitted into the helical hollow space of the rib, and said guide plate terminating shortly before the closed end of said hollow space.
  • a heat exchanger for treating moist, tacky material which comprises a. a stationary drum, having b. an internal hollow shaft or rotor with inlet and outlet for the heat exchanging medium,
  • annular bodies in the shape of ribs encircling said rotor, each of said ribs being provided with a helical, hollow space, the inner end of which communicates with the hollow shaft, the outer end being closed, and means for rotating said hollow shaft and the shaft attached annular rib shaped bodies, said annular bodies being further characterized in that the distance between the turns of the helical hollow spaceis adjusted so that helically cut strips of width substantially corresponding to the distance between the turns of said strips can be used for forming'the hollow space in a direction such that the closed end of the helical space is in front whereby movement of the condensate back to the hollow space of the rotor is aided by the rotor movement.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Drying Of Solid Materials (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
US464642A 1973-05-01 1974-04-26 Heat exchanger Expired - Lifetime US3923097A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DK235273AA DK138406B (da) 1973-05-01 1973-05-01 Tørreapparat.

Publications (1)

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US3923097A true US3923097A (en) 1975-12-02

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US (1) US3923097A (en, 2012)
JP (1) JPS5241501B2 (en, 2012)
BR (1) BR7403479D0 (en, 2012)
DD (1) DD115752A5 (en, 2012)
DE (1) DE2420662C2 (en, 2012)
DK (2) DK138406B (en, 2012)
ES (1) ES202779Y (en, 2012)
FR (1) FR2228212B3 (en, 2012)
GB (1) GB1463688A (en, 2012)
NL (1) NL7405645A (en, 2012)
PL (1) PL88803B1 (en, 2012)
SU (1) SU897121A3 (en, 2012)

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4337583A (en) * 1981-05-14 1982-07-06 Harris Kenneth R Apparatus and method for drying a substance
US4608766A (en) * 1984-06-18 1986-09-02 Kabushiki Kaisha Okawara Seisakusho Horizontal fluidized-bed dryer with heat transfer tubes
US4621684A (en) * 1985-01-22 1986-11-11 Delahunty Terry W Rotary heat exchanger with circumferential passages
US4660628A (en) * 1984-08-02 1987-04-28 Stord Bartz A/S Heat exchanger
US4666564A (en) * 1984-04-21 1987-05-19 Fried. Krupp Gesellschaft Mit Beschrankter Haftung Method of and apparatus for distilling a monoazeotropic liquid mixture
WO1989006337A1 (en) 1987-12-28 1989-07-13 Henrik Ullum Device for heating and/or drying
ES2110870A2 (es) * 1994-03-10 1998-02-16 Mc Enman S L Aparato y procedimiento para deshumectar productos en forma de pasta por evaporacion intensiva.
US5927970A (en) * 1996-10-02 1999-07-27 Onsite Technology, L.L.C. Apparatus for recovering hydrocarbons from solids
US5928678A (en) * 1990-08-31 1999-07-27 Agp, L.P. Mash feed conditioning apparatus
US5964278A (en) * 1994-05-09 1999-10-12 Kvaerner Engineering A.S Heat exchanger
US6170168B1 (en) * 1996-10-08 2001-01-09 Atlas-Stord Denmark A/S Circular drying element and drying plant with such a drying element
WO2002048628A1 (en) * 2000-12-12 2002-06-20 Atlas-Stord Denmark A/S Annular drying element, method and use hereof and drying apparatus
US20030107174A1 (en) * 2001-12-11 2003-06-12 Loewenstein David Allen Poker game
US20030136747A1 (en) * 2002-01-18 2003-07-24 Wood Bradford Russell Soil cleaning systems and methods
US20030168206A1 (en) * 2001-07-26 2003-09-11 Larsen Yngve Sten Rotary disc-type heat exchanger
US20050279715A1 (en) * 2002-01-18 2005-12-22 Strong Gary S Thermal drill cuttings treatment with weir system
US20100018671A1 (en) * 2006-10-25 2010-01-28 Nara Machinery Co., Ltd Heat exchanging device for powder, and method for manufacturing the same
CN101870550A (zh) * 2010-06-04 2010-10-27 浙江大学 双叶斜置自清式污泥真空连续干燥机
EP2832236B1 (en) 2013-07-30 2016-03-23 Tessenderlo Chemie NV Method for producing hydrolysed keratinaceous material
CN106179038A (zh) * 2016-08-31 2016-12-07 山东豪迈机械制造有限公司 一种新型可换热搅拌轴及管式反应器
US20180229197A1 (en) * 2017-02-15 2018-08-16 Wenger Manufacturing, Inc. High thermal transfer hollow core extrusion screw assembly
US10154678B2 (en) 2013-07-30 2018-12-18 Tessenderlo Chemie N.V. Method for producing hydrolysed keratinaceous material
US11412642B2 (en) * 2019-03-27 2022-08-09 Rolls-Royce Plc Heat exchanger
US11718057B2 (en) 2016-02-19 2023-08-08 Regreen Technologies, Inc. Apparatus for pressing and dehydrating of waste
US12256760B2 (en) 2017-09-08 2025-03-25 Wenger Manufacturing, LLC Method and apparatus for production of high meat content pet foods

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Publication number Priority date Publication date Assignee Title
JPS52102992A (en) * 1976-02-24 1977-08-29 Toshiba Corp Plenum for nuclear container
DK155468C (da) * 1984-10-04 1989-08-14 Atlas As Toerreapparat omfattende et stationaert hus og en rotor med et antal ringformede toerrelegemer
DK154800C (da) * 1986-04-03 1989-07-03 Atlas As Toerreapparat omfattende et stationaert hus og en rotor med et antal ringformede toerrelegemer
DK160846C (da) * 1988-11-10 1991-10-07 Atlas Ind As Roterende toerrer samt anvendelse heraf
GB9204093D0 (en) * 1992-02-26 1992-04-08 Wykes Engineering Co Rushden L Multi-disc heat exchanger
FR2940422B1 (fr) * 2008-12-19 2010-12-03 Gea Batignolles Technologies T Echangeur de chaleur comprenant des tubes a ailettes rainurees
SE534766C2 (sv) * 2010-04-26 2011-12-13 Itt Mfg Enterprises Inc Genomföring för rötkammare
CN106871604A (zh) * 2015-12-10 2017-06-20 俞扬池 一种铜粉干燥设备
RU2614304C1 (ru) * 2016-01-12 2017-03-24 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кубанский государственный аграрный университет" Аппарат теплообменный
CN105727811B (zh) * 2016-03-11 2018-01-12 无锡职业技术学院 石墨烯混合剥离系统及方法
CN110436738A (zh) * 2019-06-24 2019-11-12 吴植仁 一种加热蒸汽走平面螺旋道的圆盘
DE102023109778A1 (de) * 2023-04-18 2024-10-24 Seab Solar-Energie-Anlagenbau Gesellschaft Mbh Trocknungsvorrichtung zum Entziehen von Feuchtigkeit aus Produkten und Verfahren zum Herstellen einer Trocknungsvorrichtung
CN119258857A (zh) * 2024-12-09 2025-01-07 临汾市综合检验检测中心 一种具有加热功能的磁力搅拌器

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US230976A (en) * 1880-08-10 Milk cooler and heater
US3486740A (en) * 1967-03-02 1969-12-30 Packaged Power Terminals Inc Apparatus for treating flowable materials
US3800865A (en) * 1970-05-16 1974-04-02 Stord Bartz Industri As Heat exchanges
US3777810A (en) * 1972-08-24 1973-12-11 Strong Mfg Co Scott Dryer

Cited By (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4337583A (en) * 1981-05-14 1982-07-06 Harris Kenneth R Apparatus and method for drying a substance
US4666564A (en) * 1984-04-21 1987-05-19 Fried. Krupp Gesellschaft Mit Beschrankter Haftung Method of and apparatus for distilling a monoazeotropic liquid mixture
US4608766A (en) * 1984-06-18 1986-09-02 Kabushiki Kaisha Okawara Seisakusho Horizontal fluidized-bed dryer with heat transfer tubes
US4660628A (en) * 1984-08-02 1987-04-28 Stord Bartz A/S Heat exchanger
EP0191800B1 (en) * 1984-08-02 1988-01-13 Stord Bartz A/S Heat exchanger
US4621684A (en) * 1985-01-22 1986-11-11 Delahunty Terry W Rotary heat exchanger with circumferential passages
WO1989006337A1 (en) 1987-12-28 1989-07-13 Henrik Ullum Device for heating and/or drying
US4982514A (en) * 1987-12-28 1991-01-08 Henrik Ullum Apparatus for heating and/or drying
US5928678A (en) * 1990-08-31 1999-07-27 Agp, L.P. Mash feed conditioning apparatus
ES2110870A2 (es) * 1994-03-10 1998-02-16 Mc Enman S L Aparato y procedimiento para deshumectar productos en forma de pasta por evaporacion intensiva.
US5964278A (en) * 1994-05-09 1999-10-12 Kvaerner Engineering A.S Heat exchanger
US5927970A (en) * 1996-10-02 1999-07-27 Onsite Technology, L.L.C. Apparatus for recovering hydrocarbons from solids
US6170168B1 (en) * 1996-10-08 2001-01-09 Atlas-Stord Denmark A/S Circular drying element and drying plant with such a drying element
WO2002048628A1 (en) * 2000-12-12 2002-06-20 Atlas-Stord Denmark A/S Annular drying element, method and use hereof and drying apparatus
US20030168206A1 (en) * 2001-07-26 2003-09-11 Larsen Yngve Sten Rotary disc-type heat exchanger
US20030107174A1 (en) * 2001-12-11 2003-06-12 Loewenstein David Allen Poker game
US20040222590A9 (en) * 2001-12-11 2004-11-11 Loewenstein David Allen Poker game
US20030136747A1 (en) * 2002-01-18 2003-07-24 Wood Bradford Russell Soil cleaning systems and methods
US20050279715A1 (en) * 2002-01-18 2005-12-22 Strong Gary S Thermal drill cuttings treatment with weir system
US7306057B2 (en) 2002-01-18 2007-12-11 Varco I/P, Inc. Thermal drill cuttings treatment with weir system
US20100018671A1 (en) * 2006-10-25 2010-01-28 Nara Machinery Co., Ltd Heat exchanging device for powder, and method for manufacturing the same
US8813833B2 (en) * 2006-10-25 2014-08-26 Nara Machinery Co., Ltd. Heat exchanging device for powder, and method for manufacturing the same
CN101870550A (zh) * 2010-06-04 2010-10-27 浙江大学 双叶斜置自清式污泥真空连续干燥机
EP2832236B1 (en) 2013-07-30 2016-03-23 Tessenderlo Chemie NV Method for producing hydrolysed keratinaceous material
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DK138406B (da) 1978-08-28
ES202779Y (es) 1976-04-01
ES202779U (es) 1975-12-01
NL7405645A (en, 2012) 1974-11-05
DK138406A (en, 2012)
DK138406C (en, 2012) 1979-02-05
PL88803B1 (en, 2012) 1976-09-30
DE2420662A1 (de) 1974-11-21
GB1463688A (en) 1977-02-02
FR2228212A1 (en, 2012) 1974-11-29
JPS5241501B2 (en, 2012) 1977-10-19
BR7403479D0 (pt) 1974-12-24
SU897121A3 (ru) 1982-01-07
DD115752A5 (en, 2012) 1975-10-12
DE2420662C2 (de) 1985-09-12
JPS5027151A (en, 2012) 1975-03-20
FR2228212B3 (en, 2012) 1977-03-04

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